Specification
[0001] Conventional steam power plant plants have a closed water-steam cycle. In the steam
generator so much energy is added to the feed water by combustion of a fossil fuel
that it passes into the vaporous aggregate condition. This steam drives a generator
via one or several steam turbines and afterwards is liquefied again in a condenser.
Advantages of the invention
[0002] The invention is based on the general approach of solar-fossil hybrid power plants.
The solar system is combined with heat storage. The claimed invention comprises field
of solar collectors to collect thermal energy and a heat storage. This combination
is called in conjunction with the claimed invention "flexible solar system".
[0003] Existing hybrid pants or published concepts use solar collector power modules to
convert solar radiation into thermal energy (solar collectors) or to convert it directly
into electrical energy (photovoltaic power plants) or to support a fossil fired power
plant.
[0004] The hybridization of solar-thermal energy and a fossil-fired steam power plant combines
the advantages of both technologies: the current technical and economic advantages
of the conventional power plant and the environmental advantages of renewable energy.
Furthermore the specific investment costs of the solar system will be lower than for
a stand-alone power plant because the required water steam-cycle and infrastructures
are already available.
[0005] But without energy storage this solar energy can only be used when the solar radiation
is available. At this time this additional energy integrated in the power plant will
have to compete with comparable energy sources: solar-thermal power plants and photovoltaic
power plants.
[0006] Currently the photovoltaic panels have a really low specific costs (in €/kW
peak), which makes the integration of other solar technologies difficult. However the
electrical energy, produced by the photovoltaic panels, is currently difficult to
store in large scale and is expensive. Consequently, to avoid this competition and
to create a competitive advantage, the claimed addition of a heat storage to the solar-thermal
/ fossil fuel hybridization will allow the plant operator to use the energy collected
by the solar collectors at other time of the day (e.g. at night or during cloudy times),
when the photovoltaic panels are not in operation.
[0007] Consequently the claimed invention combines a solar field with a heat storage. The
result are lower specific investment costs compared to stand-alone solar-thermal power
plants and the possibility to use the solar energy at the needed time, which delivers
a significant advantage against the photovoltaic panels.
Description of the invention
[0008] The invention is related to the modification of an existing fossil fired power plant
to integrate solar thermal energy either at the same time it is collected or with
a certain delay of up to several hours. For economic reasons a delay of 12 hours or
less is sufficient.
[0009] This can be achieved at the low pressure preheating train or at the high pressure
preheating train. In both approaches the additional system combines a solar field
and a thermal storage system. Additionally the existing facilities of the conventional
steam water power plant are reused as much as possible.
[0010] The required collector field and the heat storage system will be arranged within
the existing power plant infrastructure and the surroundings areas.
[0011] The purpose for introducing solar thermal energy into a fossil fired power plant
is to increase the share of renewable energy and use the existing water steam cycle
including the turbo group (turbine and generator), which will bring the cost of electricity
down compared to stand alone CSP power plants.
[0012] The addition of a heat storage to this solar thermal energy integration adds the
possibility to use the solar energy at times with high electricity demand and when
other comparable renewable energies are not available (e.g. at night or times with
no wind). Further the storage system can also be loaded at times with a low load by
the condensate or feed water system with energy generated from fossil fuel.
[0013] Due to the claimed addition of a heat storage this system will not compete directly
with the photovoltaic collectors and offer the advantage that electricity can be produced
from solar radiation at the time it is needed.
[0014] The additional heat input can be either used for power output increase or for maintaining
the power output while fossil fuel is being saved.
[0015] The claimed invention brings benefits in many ways:
The utilization of existing infrastructures eliminates a cost intensive share compared
to stand alone power plants.
[0016] Furthermore the available grid connection and the existing authorization for the
power plant help for the authorization process and eliminate the dedicated costs.
[0017] The chosen integration locations (low pressure and/or high pressure) are adapted
to the existing solar technologies. Whereas the non-concentrating solar collector
technologies are working at the condensate temperature range, the concentrated solar
technologies reach temperature parameters comparable to the temperatures of the feed
water in the existing steam power plants.
[0018] The possibility to store the solar energy and to use it at times when the solar radiation
is not available makes the electricity generated economically more valuable and is
a clear advantage compared to photovoltaic panels, which does not have currently comparable
storage installations. Additionally it avoids the direct competition with these technologies
when the sun is shining.
[0019] Further advantages and advantageous embodiments of the invention can be taken from
the following drawing, its specification and the patent claims. All features described
in the drawing, its specification and the patent claims can be relevant for the invention
either taken by themselves or in optional combination with each other.
Drawings
[0020]
- Figure 1
- a first embodiment of the claimed invention (LP direct integration),
- figure 2
- a second embodiment of the claimed invention (LP indirect integration with direct
heat storage integration),
- figure 3
- a third embodiment of the claimed invention (LP indirect integration with indirect
heat storage integration),
- figure 4
- a fourth embodiment of the claimed invention (LP indirect integration and solar field
closed loop),
- figure 5
- a fifth embodiment of the claimed invention (HP direct integration),
- Figure 6
- a sixth embodiment of the claimed invention (HP indirect integration with direct heat
storage integration),
- figure 7
- a seventh embodiment of the claimed invention (HP indirect integration with indirect
heat storage integration),
- figure 8
- an eighth embodiment of the claimed invention (HP indirect integration and solar field
closed loop) and
- figure 9
- a block diagram of a conventional steam power plant (prior art).
Description of the embodiments
[0021] In figure 2 a first embodiment of a steam power plant according to the invention
is shown.
[0022] As the claimed invention essentially is concerned with the section of the steam power
plant between the condenser 5 and the steam generator 1 or an economiser 29 only this
part of the steam power plant is shown in figures 2 to ff. Neither are, for reasons
of clarity, all fittings, tubes, valves, pumps and components in figures 2 ff. are
shown or designated with reference numerals.
[0023] The illustration of the valves, tubes, fittings and components corresponds to DIN
2482 "Graphic symbols for heat diagrams", which herewith is referred to, and are thus
self-explanatory.
[0024] Since all figures are simplified illustrations of the system it may happen that not
all components are shown, but in this case a man skilled in the art may easily add
the missing component, e. g. a missing pump or the like, to the figures.
[0025] Where obviously identical connections are present several times, partially the insertion
of reference numerals is dispensed with in order to maintain the clarity of the figures.
[0026] In addition to the water-steam circuit of a conventional water steam power plant
a heat storage 11 and a solar field 13 (i. e. a field of several solar collectors)
are installed. This combination of a heat storage 11 and a solar field 13 is called
in conjunction with the claimed invention a flexible solar system 21, because it supports
the preheating system with thermal energy from the solar field 13 directly or from
the heat storage 11.
[0027] At the outlet of the heat storage a pump 12 is installed for loading and unloading
the heat storage 11.
[0028] The bypassed feedwater mass flow through the flexible solar system 21 changes based
on the energy, which can be collected by the solar field 13 and the energy demand
of the preheaters PH1 to PH6. A positive difference between the output of the solar
field 13 and the energy demand of the preheaters PH1 to PH6 can be stored in the heat
storage 8. A negative difference between the output of the solar field 13 and the
energy demand of the preheaters PH1 to PH6 is available by unloading the heat storage
8.
[0029] Since the temperature of the thermal energy that is delivered by the heat storage
8 is not necessarily a constant value, the thermal energy extracted from the heat
storage 8 may be fed into the condensation line 19 at different locations with different
operating temperatures. This makes the claimed flexible solar system more efficient
independent from the actual operating temperature of the heat storage and the load
of the turbine 3.
Figure 1: Option a) Low pressure direct integration
[0030] One of the claimed options is to integrate the thermal energy coming from the solar
field 13 at the low pressure pre-heating train, namely the prehaters PH1 to PH4.
[0031] The goal is to replace the extracted steam energy used in the pre-heating train from
the turbine 3 by the solar energy that is collected by the solar field 13. The low
pressure preheating train PH1 to PH4 is bypassed completely or partly by the additional
system as displayed in Figure 1:
A bypass inlet 15 is downstream the condensate pump 7 or at a higher temperature level
downstream an existing low pressure pre-heater PH1, PH2 or PH3 and a bypass outlet
17 is upstream the feed water pump 9 or at a lower temperature level downstream an
existing low pressure preheater. The ductwork between the bypass inlet 15 and the
bypass outlet 17 including valves that is necessary to connect the heat flexible solar
system 21 (heat storage 11 and the solar field 13) with the condensate line 19 of
the power plant does not bear reference numerals for reasons of clarity.
[0032] The condensate parameters at the bypass outlet 17 have to reach the existing parameters.
This means that the solar field 13 comprises in most cases non-concentrating solar
collectors.
[0033] The bypassed condensate mass flow changes based on the energy, which can be and/or
are wanted to be integrated.
[0034] The operation of the system depends on external parameters:
- When the solar radiations are enough to reach the final condensate parameters and this additional energy amount is needed in the existing water steam cycle, then the condensate is partly or completely bypassed
to the solar system 13, is heated up in the solar system 13 and goes back to the existing
water steam cycle via the bypass outlet 17.
- When the solar radiations are enough to reach the final condensate parameters and this additional energy amount is at present not needed in the existing water steam cycle, the solar system 13 can work in parallel to the
existing water steam cycle. In this case the energy collected by the solar field 13
is stored in the heat storage 11.
- When the solar radiations are not enough to reach the final condensate parameters and this additional energy amount is needed in the existing water steam cycle, the stored energy in the heat storage 11 can be
used. A part of the condensate mass flow is in that case bypassed and is routed to
the heat storage 8. The cold condensate replaces the stored hot condensate in the
heat storage 11. The hot condensate is routed to the existing water steam cycle. For
this option the hot condensate is routed upstream the feed water pump 9 into the condensate
line 19 via the bypass outlet 17.
- If the available solar energy is higher than the possible (or wanted) energy integration, then a part of the solar heated
condensate goes back to the existing water steam cycle via the bypass outlet 17 and
the part of the solar heated condensate is routed to the heat storage 11. The replaced
cold condensate inside the heat storage 11 is then routed to the solar field 13 in
order to be heated up again.
- If the available solar energy is lower than the possible (or wanted) energy integration,
then a part of the condensate is heated in the solar field 13 and the other part is
replaced by energy from the heat storage 11.
[0035] Following the explanations given about the function of the claimed invention a man
skilled in the art will know which valve has to be opened or closed, which pump 12,
14 has to be activated or shut down, since the figures are at least to that extent
self-explanatory.
[0036] The option a) as illustrated in figure 1 uses the same heat carrying medium, i. e.
the steam or water of the steam water circuit of the power plant(direct integration).
This reduces the heat losses and the investment costs.
[0037] These basic principles explained in conjunction with figure 1 are applicable to the
other embodiments of the claimed invention as illustrated and described in conjunction
with figures 2 to 8.
Figure 2 Option b) Low pressure indirect integration
[0038] The second embodiment comprises several concepts with the same place of the bypass
inlet 15 and the bypass outlet 17 than as figure 1 (option a)). They are displayed
in figure 2 for option b).1,
in figure 3 for option b).2 and
in figure 4 for option b).3.
[0039] The second to fourth embodiment (options
b).1 to
b).3, c. f. figures 2 to 4)comprises a heat exchanger 23 between the condensate line 19
and the solar field 13 and/or the heat stored in the heat storage 11.
[0040] This heat exchanger 23 transfers the thermal energy from the solar system 13 and
the heat storage 8 to the condensate line 19 or more generally spoken to the water
steam system of the power plant.
[0041] This separation is necessary when the medium used in the solar system 13 and the
heat storage 11 is not water, does not have the same state of aggregation (e.g vapor
instead of fluid), the same state of quality or when a separation is advantageous
for security reasons.
[0042] The system illustrated in figure 2 uses the same heat carrier for the heat storage
11 and the solar field 13 and comprises the same structure between the heat storage
tanks 11 and the solar field 13 as the first embodiment (figure 1). This is called
in conjunction with the claimed invention a direct storage integration.
[0043] The system illustrated in figure 3 comprises a further heat exchanger 25. Consequently
the heat carrier for the heat storage 11 and the solar field 13 may be different.
This is called in conjunction with the claimed invention an indirect storage integration.
A pump 14 is installed to transport the heat carrier from the solar field 13 and to
the bypass outlet 17 through the heat exchanger 25.
[0044] Depending on the medium and on the state of aggregation (vapor or fluid) of the heat
carrying medium it is in some cases technically and economically more advantageous
to have a separation between the solar field 13 and the heat storage 11 (figure 3).
In this case an additional heat exchanger 25 between this both components transfers
the energy from the solar field to the heat storage.
[0045] This system can be used in both ways: either the heat collected in the solar field
13 is transmitted to the heat storage 8, because the collected solar energy cannot
be used in the existing water steam cycle at the time of collection, because there
is not enough demand.
[0046] Alternatively the heat in the storage tanks 11 is transmitted to the fluid coming
from the solar field 13, because there is not enough solar energy collected to cover
the present energy demand in the water steam cycle.
[0047] The option b).3 displayed in figure 4 is the combination between a heat storage system
11 that is directly connected to the condensate line 19 and a closed solar system
13. To transfer the energy collected by the closed solar system or field 13 to either
the condensate line 19 or the heat storage 11 a heat exchanger 27 and a pump 14 are
provided. The collected energy from the solar field 13 is transmitted to the additional
heat exchanger 27. This thermal energy can then be transferred either directly to
the condensate line 19 (i. e. back to the existing water steam system) or to the heat
storage 11 . This option allows the use of the energy stored in the heat storage 11
without launching the solar system 13(e.g. at night).
Figure 5 Option c) High pressure direct integration
[0048] The fifth embodiment illustrated in figure 5 comprises the same solar system structure
and the same integration idea than in option a) (c. f. figure 19. The main differences
are the points where the energy from the solar field 13 and/or the heat storage 11
is fed into the water steam cycle.
[0049] The energy from the solar field 13 and/or the heat storage 11 is fed into the condensate
19 at the high pressure preheating train downstream the feed water container 8 and
upstream an economiser 29 as displayed in figure 5: the bypass inlet 15 location is
downstream the boiler feed pump 9 and the bypass outlet 17 is downstream the last
high pressure preheater PH6. The bypass inlet 15 and outlet 17 can be adapted to the
optimal operation temperature of the solar field 13 by changing the integration location
within the high pressure preheating train.
[0050] A single HP-preheater PH5 or more than one HP-preheater PH5, PH6 can be bypassed
depending on the temperature level wanted.
[0051] The solar system, comprising of the solar field 13 and the heat storage 11 for solar
energy replaces then the existing pre-heating train (PH5, PH6) partially or completely
and consequently the energy of the extracted steam from the high pressure part 3.1
of the turbine 3.
Figure 6 Option d) High pressure indirect integration
[0052] The sixth to eights embodiments are illustrated in figures 6 to 8 and comprise the
same integration location than the fifth embodiment and the same integration concept
than in option b) (c. f. figures 2 to 4). They are displayed
in figure 6 for option d).1,
in figure 7 for option d).2 and in
in figure 8 for option d). 3.
[0053] The difference is that the solar energy is indirectly integrated or fed into the
steam water circuit. An additional heat exchanger 31 transfers the thermal energy
from the solar system, comprising of the solar field 13 and the heat storage 11, to
the feed water system of the steam power plant. This separation is necessary when
the medium used in the solar system is not water, does not have the same state (e.g.
vapor instead of fluid), same quality or when a separation is advantageous for security
reasons.
[0054] The differentiation between option d).1 and d).2 (c. f. figure 7) is the direct or
the indirect integration of the heat storage 11 in the solar system. Depending on
the medium and on the medium state of aggregation (vapor or fluid) it is in some cases
technically and economically more advantageous to have a separation between the solar
field and the heat storage (option d).2).
[0055] In this case an additional heat exchanger 33 between the heat storage 11 and the
solar field 13 transfers the energy from the solar field 13 to the heat storage 11
is installed. This system can be used in both ways: either the heat in the solar field
13 is transmitted to the heat storage 11, because the collected solar energy cannot
be integrated in the existing water steam cycle, due to a lack of demand.
[0056] Alternatively the heat stored in the storage tanks 11 is transmitted to the fluid
coming from the solar field 13, to raise its temperature, because there is not enough
solar energy available to satisfy the energy demand of the water steam cycle.
[0057] The option d).1 comprises the same structure between the heat storage tanks and the
solar field than in option c).
[0058] The option d).3 displayed in figure 8 is combination of a heat storage system 11
directly connected to the feed water preheating system PH5, PH6 or the condensate
line 19 and a closed solar system (indirect integration). The energy from the solar
field 13 is transmitted to an additional heat exchanger 35. This energy can then be
transferred either directly to the feed water preheating system (back to the existing
system) or to the storage tank 11. It is still possible to use the energy stored in
the heat storage 11 without launching the solar system 13 (e.g. at night).
[0059] In figure 9 a conventional steam power plant fuelled with fossils or biomass is represented
as block diagram. Figure 1 essentially has the purpose of designating the components
of the power plant and to represent the water-steam-cycle in its entirety. For reasons
of clarity in the following figures only those parts of the water-steam-cycle are
represented which are essential to the invention.
[0060] In a steam generator 1 under utilization of fossil fuels or biomass live steam is
generated out of the feed water. The live steam is expanded in a steam turbine 3 and
thus drives a generator G. Turbine 3 can be separated into a high-pressure part HP,
a medium-pressure part MP and a low-pressure part LP.
[0061] After expanding the steam in turbine 3, it streams into a condenser 5 and is liquefied
there. For this purpose a generally liquid cooling medium, as e. g. cooling water,
is supplied to condenser 5. This cooling water is then cooled in a cooling tower (not
shown) or by a river in the vicinity of the power plant (not shown), before it enters
into condenser 5.
[0062] The condensate originated in condenser 5 is then supplied, by a condensate pump 7,
to several preheaters PHi, with i = 1 ... n. In the shown embodiment downstream second
preheater PH2 a feed water container 8 is arranged. The feed water container 8 may
comprise a third preheater PH3. Behind the feed water container 8 a feed water pump
9 is provided.
[0063] In combination with the invention it is of significance that the condensate from
condenser 5 is preheated with steam beginning with the first preheater PH1 until the
last preheater PH5. The tapping steam is taken from turbine 3 and leads to a diminution
of the output of turbine 3. With the heat exchange between tapping steam and condensate
the temperature of the condensate increases from preheater to preheater. Consequently
the temperature as well of the steam utilized for preheating must increase from preheater
to preheater.
[0064] In figure 9 the preheaters PH1 and PH2 are heated with steam from low-pressure part
LP of steam turbine 3, whereas the last preheater PH5 is partially heated with steam
from the high-pressure part HP of steam turbine 3. The third preheater PH3 arranged
in the feed water container 8 is heated with steam from the medium-pressure part MP
of turbine 3.
1. Steam power plant comprising a steam generator (1), a turbine (3), a condenser (5),
a feed water container (8), a condensate line (19) at least one low-pressure preheater
(PH1 to PH4)and at least one high-pressure preheater (PH5, PH6), wherein the condensate
line (19) connects the condenser (5), the preheaters (PH1 to PH6) and the feed water
container (8) with each other, characterized in that it comprises a flexible solar system (21) and that the flexible solar system (21)
is mounted parallel to the condensate line (19).
2. Steam power plant according to claim 1, characterized in, that the flexible solar system (21) comprises a heat storage (11) and a field of solar
collectors (13).
3. Steam power plant according to claim 2, characterized in, that the solar collectors (13) may be concentrating and/or non-concentrating.
4. Steam power plant according to one of the foregoing claims, characterized in, that the flexible solar system (21) is mounted parallel to one or more of the low pressure
preheaters (PH1, PH2, PH3, PH4).
5. Steam power plant according to one of the foregoing claims, characterized in, that the flexible solar system (21) is mounted parallel to one or more of the high pressure
preheaters (PH5, PH6).
6. Steam power plant according to one of the foregoing claims, characterized in, that the flexible solar system (21) comprises a ductwork and several valves and pumps
that flexibly allow to bypass one or more of the preheaters (PH1 to PH6) depending
on temperature of the thermal energy delivered by the flexible solar system (21).
7. Steam power plant according to one of the foregoing claims, characterized in, that the flexible solar system (21) delivers thermal energy from the solar field (13)
and the heat storage (11) simultaneously to the condensate line (19).
8. Steam power plant according to claim 1, characterized in, that the flexible solar system (21) delivers thermal energy from the solar field (13)
and the heat storage (11) simultaneously to the condensate line (19) at different
temperatures to different preheaters.
9. Steam power plant according to one of the foregoing claims, characterized in, that the flexible solar system (21) is directly connected to the condensate line (19).
10. Steam power plant according to one of the claims 1 to 9, characterized in, that between the flexible solar system (21) and the condensate line (19) a heat exchanger
(23, 31) is mounted.
11. Steam power plant according to one of the foregoing claims, characterized in, that the heat storage (11) is indirectly connected to the flexible solar system (21) by
means of a heat exchanger (25, 33).
12. Steam power plant according to one of the foregoing claims, characterized in, that the solar field (13) is indirectly connected to the flexible solar system (21) by
means of a heat exchanger (27, 35).
13. Steam power plant according to one of the foregoing claims, characterized in that the flexible solar system (21) comprises at least one pump (12, 14).
14. Method of operating a steam power plant according to one of the foregoing claims,
comprising the steps of
Heating up a fluid energy carrier by means of the solar field (13) and
delivering this energy carrier to the condensate line (19) and/or the heat storage
(11) depending on the energy demand of the preheaters (PH1 to PH6) in the condensate
line (19) and the charge of the heat storage (11).
15. Method according to claim 14 characterized in that, the flexible solar system (21) may deliver thermal energy form the heat storage
(11) and/or the solar field (13) to the preheaters (PH1 to PH6) in the condensate
line (19).
16. Method according to claim 14 or 15 characterized in that, the heat storage (11) m is loaded with thermal energy from the condensate line (19).